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This informative blog allows plastics professionals to discuss plastics training and technology. Brought to you by Routsis Training: the plastic industry's premiere training provider.

DECOUPLED-I vs. DECOUPLED-II Process…

I received this question the other day…

Rafael
In a D1 (DECOUPLED MOLDING 1) process the first stage is filling and packing, yet a D2 process isolates filling in the first stage. Could you please explain the difference?
My Response
In a D1 process, the mold cavity is completely filled using velocity controlled first stage. The second stage is mainly used to compensate for shrinkage and wait until the gate freezes.
In a D2 process, the mold cavity is not completely filled using velocity controlled first stage (visible short). The second stage is used to finish mold filling, compensate for shrinkage, and wait for gate freeze.
Additional Thoughts
Although the the velocity controlled injection of the D1 process is better than the traditional pressure-controlled injection of older molding machines, it still places too much material into the mold during 1st stage. In reality, most injection molding processes benefit from a short shot during 1st stage using a D2 process.
-Andy

Purpose of Reverse Temperature Profiling

I got this question and felt it would make a good discussion on the blog…

Larry
Where and why is a reverse profile barrel temperature used?
My Response
A reverse profile is typically used when processing materials such as nylon and LCP. In fact it is quite common for many semi-crystalline polymers. Basically, such polymers have a melting point. The high rear temperature often helps improve conveyance as well as melt the polymer quickly, Once melted, the polymer can often be cooled a little in the front to improve the overall cycle time and meet the desired melt temperature.
Usually the need for a forward or reverse temperature profile should be approached scientifically. The middle barrel temperatures should be set to the desired melt temperature. The front zones are typically adjusted to obtain the desired melt temperature. The rear temperature should be set  to optimize feed and melt consistency.
Historically, low viscosity polymers with high crystallinity tend to process best using a reverse profile… but you should always look to optimize this, since everyone has different screws, barrel, heater bands, thermocouples, and temperature controllers.
Additional Thoughts
Try not to confuse the front temperature with the actual nozzle temperature. The nozzle temperature will be adjusted independently to meet the needs of the specific process, such as avoiding drool or freeze off.
-Andy

Training While Things Are Slow…

I just heard another common excuse for not training…

HR Manager
We are waiting until things pick up before we start employee training.
My Thoughts
Believe it or not, slow times are the optimal time to start your employee training initiative. These are great opportunities to get your current employees up to speed, and prepare them for the next increase in production.
This is especially true if you hire temporary employees since you will rely heavily on your current employees to being new and temporary hires up to speed when things get busy.
-Andy

The Purpose of Cushion

I just received this question regarding a recent posting on my blog…

Blog Reader
You mentioned pressure loss with respect to the importance of maintaining a consistent cushion, could you quickly expand that thought?

My Response
All plastics are compressible… therefore there is a compression that takes place with the polymer in front of the screw. There needs to be a cushion to compensate for variability, but too much cushion results in too much pressure loss before the nozzle.
Additional Thoughts
Although a consistent cushion will help ensure a more reliable process… cushion control is not a reliable method of achieving this. You are best to monitor the cushion and adjust the shot size and transfer yourself when necessary.
-Andy

Understanding Back-Flow Within the Mold…

I received this question yesterday…

MJ
Could you explain the phenomena of back-flow inside the mold? I have in-mold sensors, but I don’t think I am seeing this.
My Response
Basically, there are two areas within the molding process where back-flow typically occurs:
1) Transfer From Fill To Pack: If the mold is completely full during first stage, the mold will begin to pressurize as the machine tries to continue pack the mold with first stage fill. When the machine transfers to pack using a lower pressure, a little amount of the pressurized material within the mold will tend to back-flow. In some cases, this back flow will cause sinks or voids on the molded part… in other cases, you may see delamination occur. If you are using a pressure monitoring system, you may see a sharp drop in cavity pressure at the point where the machine transfers from fill to pack, especially near the gate.
2) At The End Of Pack: Insufficient packing time results in a gate which is not completely sealed. As a result, some of the pressure in the mold cavity will become relieved by a small back-flow of material across the gate into the runner system. This most often results in sinks or voids near the gate area. If you are using a pressure monitoring system, you should see a significant drop in pressure at the cavity pressure sensor near the gate when the packing pressure times out.
Additional Thoughts
Keep in mind… if your process is properly established, you should notice a nice gradual rise and fall of pressure within the mold cavity and little to no back-flow within the mold cavity.
-Andy